US4815092A - Laser generator with zeolitic catalyst carrier and method of making same - Google Patents
Laser generator with zeolitic catalyst carrier and method of making same Download PDFInfo
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- US4815092A US4815092A US07/129,528 US12952887A US4815092A US 4815092 A US4815092 A US 4815092A US 12952887 A US12952887 A US 12952887A US 4815092 A US4815092 A US 4815092A
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- laser
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- 239000003054 catalyst Substances 0.000 title claims abstract description 27
- 238000004519 manufacturing process Methods 0.000 title 1
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 claims abstract description 12
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical group O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 30
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 23
- 230000015556 catabolic process Effects 0.000 claims description 8
- 238000006731 degradation reaction Methods 0.000 claims description 8
- 239000001569 carbon dioxide Substances 0.000 claims description 7
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical group [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 claims description 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 230000000717 retained effect Effects 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 229910052759 nickel Inorganic materials 0.000 claims description 2
- 229910052709 silver Inorganic materials 0.000 claims description 2
- 239000004332 silver Substances 0.000 claims description 2
- 239000011148 porous material Substances 0.000 claims 3
- 239000008380 degradant Substances 0.000 claims 2
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims 1
- IVMYJDGYRUAWML-UHFFFAOYSA-N cobalt(ii) oxide Chemical class [Co]=O IVMYJDGYRUAWML-UHFFFAOYSA-N 0.000 claims 1
- 239000010457 zeolite Substances 0.000 abstract description 14
- 229910021536 Zeolite Inorganic materials 0.000 abstract description 12
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 abstract description 12
- 239000008187 granular material Substances 0.000 abstract description 7
- 230000003197 catalytic effect Effects 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 6
- 239000007789 gas Substances 0.000 description 30
- 238000006555 catalytic reaction Methods 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000012286 potassium permanganate Substances 0.000 description 4
- 239000005751 Copper oxide Substances 0.000 description 3
- 229910000431 copper oxide Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000005086 pumping Methods 0.000 description 3
- 239000011949 solid catalyst Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 229910000365 copper sulfate Inorganic materials 0.000 description 2
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- -1 precisely Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 229910052738 indium Inorganic materials 0.000 description 1
- APFVFJFRJDLVQX-UHFFFAOYSA-N indium atom Chemical compound [In] APFVFJFRJDLVQX-UHFFFAOYSA-N 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
Images
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01S—DEVICES USING THE PROCESS OF LIGHT AMPLIFICATION BY STIMULATED EMISSION OF RADIATION [LASER] TO AMPLIFY OR GENERATE LIGHT; DEVICES USING STIMULATED EMISSION OF ELECTROMAGNETIC RADIATION IN WAVE RANGES OTHER THAN OPTICAL
- H01S3/00—Lasers, i.e. devices using stimulated emission of electromagnetic radiation in the infrared, visible or ultraviolet wave range
- H01S3/02—Constructional details
- H01S3/03—Constructional details of gas laser discharge tubes
- H01S3/036—Means for obtaining or maintaining the desired gas pressure within the tube, e.g. by gettering, replenishing; Means for circulating the gas, e.g. for equalising the pressure within the tube
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/076—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01S—DEVICES USING THE PROCESS OF LIGHT AMPLIFICATION BY STIMULATED EMISSION OF RADIATION [LASER] TO AMPLIFY OR GENERATE LIGHT; DEVICES USING STIMULATED EMISSION OF ELECTROMAGNETIC RADIATION IN WAVE RANGES OTHER THAN OPTICAL
- H01S3/00—Lasers, i.e. devices using stimulated emission of electromagnetic radiation in the infrared, visible or ultraviolet wave range
- H01S3/02—Constructional details
- H01S3/03—Constructional details of gas laser discharge tubes
Definitions
- the present invention relates to a laser generator comprising a resonant cavity filled with a laser gas and electric pumping electrodes for causing a laser discharge in the gas of the cavity then subjected to a temperature rise.
- Such a generator is used for example in medical or military fields.
- Such degradation of the gas may be prevented by using solid catalysts disposed in the cavity, which promote the reverse chemical reactions.
- Degradation of the gas may further be prevented by adopting an active cathode, having a certain catalytic and oxidizing power, formed form an appropriate mixture of metals and oxides, such for example as copper, nickel, cobalt.
- an active cathode having a certain catalytic and oxidizing power, formed form an appropriate mixture of metals and oxides, such for example as copper, nickel, cobalt.
- hopcalite the product known under the name of hopcalite is already known. It is a mixture of manganese dioxide and copper oxide.
- the manganese dioxide oxide plays an oxidizing role and the copper oxide a catalysis role.
- this material In order to ensure the catalytic action, this material must have a particular structure, in the case in point a sponge structure.
- Hopcalite is a friable material generator of dust prejudicial to the correct operation of the laser.
- agglomerated grains of hopcalite bonded to a support, inside the laser cavity do not produce any catalysis effect.
- zeolites There further exist molecular cells with microporous structure, known under the name of zeolites. These are natural or artificial alumino-silicates. They have been used up to present as vacuum agents, because of their characteristic of retaining in their micropores very large amounts of gas and more especially heavy gases, such as precisely, carbon dioxide gas CO 2 .
- EP-A-No. 0 081 081 teaches, for a laser generator, to dispose a catalyst supporting layer in a chamber separated from the laser cavity itself. But this supporting layer extends relatively far from the laser cavity, so that it is necessary to provide means for heating the catalyst, which is a disadvantage.
- the present invention provides then a laser generator of the above mentioned type, in which the catalyst is received on a support disposed in a part of the generator communicating with the cavity, the catalyst containing manganese dioxide formed directly, on a zeolitic support, first of all by dipping the support in a first bath of potassium permanganate dissolved in water and in a second bath of metal sulfate dissolved in water, then by decomposition of the potassium permanganate in an acetone vapor atmosphere, and the zeolitic support is disposed in a hot part of the generator communicating, on the one hand, with the cavity and, on the other, with a laser gas reserve.
- the catalyst of the generator of the invention has great cohesion and, because of that, it may be disposed very close to the laser cavity, even between this cavity and the gas reserve, which avoids having to heat it.
- the zeolitic support retains the product of the permanent catalysis reaction, in this case CO 2 if the active medium of the laser is formed by a mixture comprising carbon dioxide gas, and frees it under the action of the heat. In fact, absorption and release of the carbon dioxide gas take place concomitently and permanently during operation of the generator. It is by capillary action that the gas is retained in the micropores of the zeolitic support and, when the temperature rises, this gas capillary action decreases because of the increase in the fluidity of the gas, which causes release thereof.
- the support for the catalyst of the invention acts then as a gas reservoir which is filled under the action of the increase in gas pressure in the laser cavity, and that of the laser effect and of the catalysis reaction, and which empties into the laser cavity under the action of the heat.
- FIGURE shows a schematical sectional view of the generator.
- the laser generator shown in the FIGURE comprises an outer housing 1 defining inside a duct 2 which, associated with two mirrors 4 and 5, forms a resonant cavity 3.
- This cavity is filled with a gas medium which, in the case in point, is formed by carbon dioxide gas CO 2 in fact mixed with other gases, for example CO, nitrogen, and helium.
- a gas medium which, in the case in point, is formed by carbon dioxide gas CO 2 in fact mixed with other gases, for example CO, nitrogen, and helium.
- the generator uses electric pumping and therefore comprises, not shown, a power supply source and two electrodes. They may be electrodes extending into duct 2, in the vicinity of the two mirrors 4, 5 and between which is created an electric discharge, or a thread like electrode for one and a strip electrode for the other extending over the length and on each side of the duct 2, respectively. Electric pumping is advantageously provided at a high DC voltage, but could also be effected at radio frequency.
- the invention in fact supplies to a generator with any duct, capillary or not, and that it is not limited to a gas medium comprising CO 2 .
- the invention applies to a generator having a materially defined and heating cavity.
- Housing 1 is adapted to define an extension 6, here in the form of a cylindrical sleeve with an axis perpendicular to that of the resonant cavity 3 which, in operation, also forms a hot part of the generator.
- Sleeve 6 is connected to the rest of housing 1 by an annular shoulder 7, serving as support for a catalytic cartridge 8.
- cavity 3 communicates with a reserve of the gas medium 9, inside an enclosure 10 connected to sleeve 6 by an annular shoulder 11, with interpositioning of an indium seal 12, and by means of conventional clamping means, not shown.
- the catalytic cartridge 8 comprises a perforated or latticed case 13, serving as mechanical filter and containing zeolite granules 14 on which a catalyst has been previously fixed, in the way described below.
- the zeolite granules are finally placed in an acetone vapor atmosphere, which decomposes the potassium permanganate and the copper sulfate, so as to form manganese dioxide and copper oxide which are to provide the oxidization function and the catalysis function, respectively.
- the catalyst thus obtained will have to be activated by heating to about 200° C. in a dry air stream.
- silver or cobalt may replace the copper (hopcalite) and that even several of these metals could be associated together for providing the catalysis function.
- the catalyst transforms the carbon monoxide produced by the laser effect into carbon dioxide gas CO 2 , and the micropores of the zeolite granules retain the carbon dioxide gas for releasing it under the action of the heat.
- the catalyst incorporated in the zeolite granules transforms the CO into CO 2 which is retained in the granules;
- the zeolite granules under the action of the heat, release the CO 2 and the CO 2 pressure in the cavity increases.
- the catalysis action is associated with an absorption-desorption action due, on the one hand, to the selectivity of the absorption of the zeolite, preponderant for CO 2 and, on the other hand, to the reduction of the capillarity effect on the zeolite at high temperatures.
- the hot CO 2 desorption stabilizes its output power and ensures correct operation when hot, while extending the lifespan thereof.
- the balance of the gain will depend on the microporosity of the zeolite and on the amount of catalyst material incorporated in the zeolite, which will therefore have to be experimentally but easily determined as a consequence.
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- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Engineering & Computer Science (AREA)
- Plasma & Fusion (AREA)
- Optics & Photonics (AREA)
- Crystallography & Structural Chemistry (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Lasers (AREA)
- Catalysts (AREA)
Abstract
A laser generator with a catalyst for the laser gas is provided comprising a cavity which communicates with a housing receiving a catalytic cartridge, which communicates also with a laser gas reserve, and which is subjected to the action of the heat released by the laser effect. The cartridge contains, inside a mechanical filter, granules of zeolite on which a manganese dioxide catalyst has been fixed. The generator, whose output power is stabilized, has a long lifespan.
Description
This is a continuation of Ser. No. 801,043 filed Nov. 22, 1985, now abandoned.
1. Field of the Invention
The present invention relates to a laser generator comprising a resonant cavity filled with a laser gas and electric pumping electrodes for causing a laser discharge in the gas of the cavity then subjected to a temperature rise.
Such a generator is used for example in medical or military fields.
2. Description of the Prior Art
Generators of this type have a major drawback which limits their lifespan, namely the degradation of the gas.
Degradation of the gas, generally CO2, results in the following chemical reactions, caused directly by the high voltage discharge:
CO.sub.2 →CO+O
CO→C+O
Such degradation of the gas may be prevented by using solid catalysts disposed in the cavity, which promote the reverse chemical reactions.
C+O→CO
CO+O→CO.sub.2
But the solid catalysts known up to present, such for example as hopcalite, are powdery; despite very stringent precautions during use, they therefore pollute the laser.
Degradation of the gas may further be prevented by adopting an active cathode, having a certain catalytic and oxidizing power, formed form an appropriate mixture of metals and oxides, such for example as copper, nickel, cobalt. Although such an electrode effectively prevents degradation of the gas, it causes on the other hand appreciable pollution of the resonant cavity by deposition of metals and oxides on its internal wall, thus causing another form of degradation of the laser.
Finally, and even with known solid catalysts or an active electrode, the lifespan of the generator and its correct operation remain limited.
The applicant has then tackled this problem of degradation of the laser gas and pollution of the cavity.
As catalysis means perfectly appropriate for the reaction
CO→CO.sub.2
the product known under the name of hopcalite is already known. It is a mixture of manganese dioxide and copper oxide. The manganese dioxide oxide plays an oxidizing role and the copper oxide a catalysis role.
In order to ensure the catalytic action, this material must have a particular structure, in the case in point a sponge structure.
Hopcalite is a friable material generator of dust prejudicial to the correct operation of the laser.
In any case, agglomerated grains of hopcalite bonded to a support, inside the laser cavity, do not produce any catalysis effect.
As for the solution of disposing grains of hopcalite inside a filter, it has the drawback that the filter forms, for the gases, an obstacle difficult to cross.
There further exist molecular cells with microporous structure, known under the name of zeolites. These are natural or artificial alumino-silicates. They have been used up to present as vacuum agents, because of their characteristic of retaining in their micropores very large amounts of gas and more especially heavy gases, such as precisely, carbon dioxide gas CO2.
After studying the reasons for this quality of zeolites, the applicant had the idea of using them in laser generators as supports for catalysts of the hopcalite type, despite the fact that their gas retention property has been up to now considered a disadvantage for lasers.
The document EP-A-No. 0 081 081 teaches, for a laser generator, to dispose a catalyst supporting layer in a chamber separated from the laser cavity itself. But this supporting layer extends relatively far from the laser cavity, so that it is necessary to provide means for heating the catalyst, which is a disadvantage.
The present invention provides then a laser generator of the above mentioned type, in which the catalyst is received on a support disposed in a part of the generator communicating with the cavity, the catalyst containing manganese dioxide formed directly, on a zeolitic support, first of all by dipping the support in a first bath of potassium permanganate dissolved in water and in a second bath of metal sulfate dissolved in water, then by decomposition of the potassium permanganate in an acetone vapor atmosphere, and the zeolitic support is disposed in a hot part of the generator communicating, on the one hand, with the cavity and, on the other, with a laser gas reserve.
The catalyst of the generator of the invention has great cohesion and, because of that, it may be disposed very close to the laser cavity, even between this cavity and the gas reserve, which avoids having to heat it.
The zeolitic support retains the product of the permanent catalysis reaction, in this case CO2 if the active medium of the laser is formed by a mixture comprising carbon dioxide gas, and frees it under the action of the heat. In fact, absorption and release of the carbon dioxide gas take place concomitently and permanently during operation of the generator. It is by capillary action that the gas is retained in the micropores of the zeolitic support and, when the temperature rises, this gas capillary action decreases because of the increase in the fluidity of the gas, which causes release thereof. The support for the catalyst of the invention acts then as a gas reservoir which is filled under the action of the increase in gas pressure in the laser cavity, and that of the laser effect and of the catalysis reaction, and which empties into the laser cavity under the action of the heat.
This release of gas, which increases the gain of the laser, offsets the loss of gain due to the temperature rise.
What is remarkable in the use of the zeolitic support of the invention, is that it plays a role the opposite of what is played up to present, when it was used only for filling and not for emptying.
The invention will be better understood from the following description of the preferred embodiment of the generator of the invention, with reference to the single accompanying FIGURE which shows a schematical sectional view of the generator.
The laser generator shown in the FIGURE comprises an outer housing 1 defining inside a duct 2 which, associated with two mirrors 4 and 5, forms a resonant cavity 3.
This cavity is filled with a gas medium which, in the case in point, is formed by carbon dioxide gas CO2 in fact mixed with other gases, for example CO, nitrogen, and helium.
The generator uses electric pumping and therefore comprises, not shown, a power supply source and two electrodes. They may be electrodes extending into duct 2, in the vicinity of the two mirrors 4, 5 and between which is created an electric discharge, or a thread like electrode for one and a strip electrode for the other extending over the length and on each side of the duct 2, respectively. Electric pumping is advantageously provided at a high DC voltage, but could also be effected at radio frequency.
It will be noted that the invention in fact supplies to a generator with any duct, capillary or not, and that it is not limited to a gas medium comprising CO2. Generally, the invention applies to a generator having a materially defined and heating cavity.
Housing 1 is adapted to define an extension 6, here in the form of a cylindrical sleeve with an axis perpendicular to that of the resonant cavity 3 which, in operation, also forms a hot part of the generator.
Through the sleeve 6, serving then as housing receiving cartridge 8, cavity 3 communicates with a reserve of the gas medium 9, inside an enclosure 10 connected to sleeve 6 by an annular shoulder 11, with interpositioning of an indium seal 12, and by means of conventional clamping means, not shown.
The catalytic cartridge 8, comprises a perforated or latticed case 13, serving as mechanical filter and containing zeolite granules 14 on which a catalyst has been previously fixed, in the way described below.
Starting with a commercial zeolite, which is very water absorbent, it is heated for drying it. Then it is dipped in a first bath obtained by dissolving potassium permanganate in water and it is again dried. Then it is dipped in a second bath obtained by dissolving copper sulfate in water, and it is again dried.
The zeolite granules are finally placed in an acetone vapor atmosphere, which decomposes the potassium permanganate and the copper sulfate, so as to form manganese dioxide and copper oxide which are to provide the oxidization function and the catalysis function, respectively.
Then rinsing is carried out. Before use, the catalyst thus obtained will have to be activated by heating to about 200° C. in a dry air stream.
It should be noted here that silver or cobalt, for example, may replace the copper (hopcalite) and that even several of these metals could be associated together for providing the catalysis function.
From the functional point of view, the catalyst transforms the carbon monoxide produced by the laser effect into carbon dioxide gas CO2, and the micropores of the zeolite granules retain the carbon dioxide gas for releasing it under the action of the heat.
Under the operating conditions of the laser, the following steps occur:
under the action of the laser effect, the cavity heats up and the CO2 is transformed into CO.
the catalyst incorporated in the zeolite granules transforms the CO into CO2 which is retained in the granules;
the zeolite granules, under the action of the heat, release the CO2 and the CO2 pressure in the cavity increases.
It will be noted that maintenance of the CO2 pressure in the cavity at a high level results from the catalytic action. In the absence of catalyst, a natural CO/CO2 balance would be created with an inappropriate proportion of CO2 and in any case smaller than in the presence of the catalyst.
The advantages of the above described invention are numerous.
It brings into play a clean catalyst, because of the mechanically stronger structure of the support used.
In the case of a CO2 laser, the one which was considered above, the catalysis action is associated with an absorption-desorption action due, on the one hand, to the selectivity of the absorption of the zeolite, preponderant for CO2 and, on the other hand, to the reduction of the capillarity effect on the zeolite at high temperatures.
Since the gain of a laser drops with the temperature, the hot CO2 desorption stabilizes its output power and ensures correct operation when hot, while extending the lifespan thereof. Of course, the balance of the gain will depend on the microporosity of the zeolite and on the amount of catalyst material incorporated in the zeolite, which will therefore have to be experimentally but easily determined as a consequence.
Finally, it follows from the use of zeolite as a catalyst support that there is no longer need of the device for cooling the laser which is normally indispensable.
Claims (8)
1. An arrangement for increasing the working lifetime of a gas laser, comprising:
(a) laser means for generating an output laser beam during laser discharge of a lasing gas medium contained in a resonant cavity of a main elongated housing with attendant heating of said gas medium and with degradation of said gas medium into gaseous degradants;
(b) a catalyst for converting said gaseous degradants to a reconverted gas medium during laser discharge;
(c) carrier means including a microporous zeolitic support for supporting said catalyst thereon, said microporous porous zeolitic support having gas reservoir pores for adsorbingly retaining said reconverted gas medium produced by said catalyst, and for releasing said reconverted gas medium retained in said pores when exposed to heat; and
(d) means for positioning said zeolitic support and said catalyst thereon in an elongated casing which extends transversely away from said main housing and in thermal proximity with said resonant cavity and in thermal communication with said gas medium therein such that said zeolitic support and said catalyst are heated by said gas medium during laser discharge, thereby releasing said reconverted gas medium retained in said pores of said microporous support.
2. The arrangement as recited in claim 1, wherein said casing extends perpendicularly to said main elongated housing.
3. The arrangement as recited in claim 1, wherein said casing is a tubular sleeve having constantly open opposite ends, one of which opens into said main elongated housing; and wherein said laser means includes a gas reserve enclosure which opens into said other end of said sleeve.
4. The arrangement as recited in claim 3, wherein said positioning means includes a perforated cartridge having an interior in which said support and said catalyst means are contained, said cartridge being mounted within said tubular sleeve intermediate said opposite ends thereof.
5. The arrangement as recited in claim 4, wherein said positioning means includes an annular shoulder within said sleeve and having a support surface on which said cartridge is seated.
6. The arrangement as recited in claim 1, wherein said lasing gas medium is carbon dioxide gas.
7. The arrangement as recited in claim 1, wherein said catalyst includes at least one oxide selected from the group of copper, nickel, silver and cobalt oxides.
8. The arrangement as recited in claim 1, wherein said catalyst is activated copper oxide and manganese dioxide.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR8417886A FR2575869B1 (en) | 1984-11-23 | 1984-11-23 | LASER GENERATOR WITH LASER GAS CATALYST |
| FR8417886 | 1984-11-23 |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US06801043 Continuation | 1985-11-22 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4815092A true US4815092A (en) | 1989-03-21 |
Family
ID=9309886
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/129,528 Expired - Fee Related US4815092A (en) | 1984-11-23 | 1987-12-07 | Laser generator with zeolitic catalyst carrier and method of making same |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US4815092A (en) |
| EP (1) | EP0188138B1 (en) |
| DE (1) | DE3572754D1 (en) |
| FR (1) | FR2575869B1 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4905249A (en) * | 1989-01-06 | 1990-02-27 | Applied Photonics, Inc. | Catalytic converter |
| DE3923745A1 (en) * | 1989-07-18 | 1991-01-31 | Eltro Gmbh | LASER DEVICE WITH RAMAN CELL |
| WO1996022825A1 (en) * | 1995-01-27 | 1996-08-01 | Purafil, Inc. | Improved fiber filter and methods of use thereof |
| US6125131A (en) * | 1994-10-13 | 2000-09-26 | Advanced Technology Materials, Inc. | Laser system utilizing sorbent-based gas storage and delivery system |
| US6605558B2 (en) | 1997-02-11 | 2003-08-12 | Fred Klatte | Composition for producing chlorine dioxide |
| US20030179798A1 (en) * | 2002-03-25 | 2003-09-25 | Fanuc Ltd. | Laser oscillator |
| US20040051080A1 (en) * | 2002-09-13 | 2004-03-18 | Ica Trinova, Llc | Composition and method for producing carbon dioxide |
| US6940886B2 (en) * | 2000-03-31 | 2005-09-06 | Mitsubishi Denki Kabushiki Kaisha | Laser oscillator |
| US7758836B1 (en) | 2009-04-14 | 2010-07-20 | Huggins Ronald G | System and method for removing sulfur-containing contaminants from indoor air |
| US9382116B2 (en) | 2013-01-10 | 2016-07-05 | Ica Trinova, Llc | Mixtures for producing chlorine dioxide gas in enclosures and methods of making the same |
| US10850981B2 (en) | 2017-04-25 | 2020-12-01 | Ica Trinova, Llc | Methods of producing a gas at a variable rate |
| US11912568B2 (en) | 2018-03-14 | 2024-02-27 | Ica Trinova, Llc | Methods of producing a gas at a controlled rate |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5407651A (en) * | 1991-02-15 | 1995-04-18 | Tosoh Corporation | Catalyst for and method of purifying exhaust gas |
| US5833739A (en) * | 1992-11-13 | 1998-11-10 | Klatte; Fred | Chemically coated zeolite and method for chemically coating zeolite and using coated zeolite |
| US5567405A (en) * | 1992-11-13 | 1996-10-22 | Klatte Inc. | Method for producing chlorine dioxide using chemically impregnated zeolite |
| US5573743A (en) * | 1992-11-13 | 1996-11-12 | Klatte Inc. | Method for producing chlorine dioxide and removing chlorine dioxide using chemically impregnated zeolite |
| US5278112A (en) * | 1992-11-13 | 1994-01-11 | Fred Klatte | Chemically impregnated zeolite and method for chemically impregnating and coating zeolite |
| US5464598A (en) * | 1992-11-13 | 1995-11-07 | Klatte; Fred | Method for removing a contaminant from a fluid using a chemically impregnated and coated zeolite |
| US5730948A (en) * | 1992-11-13 | 1998-03-24 | Klatte Inc. | Method for producing chlorine dioxide using chemically impregnated zeolite |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4547886A (en) * | 1981-09-25 | 1985-10-15 | United Technologies Corporation | Catalyzed sealed-off CO2 laser |
| US4617668A (en) * | 1982-07-02 | 1986-10-14 | Raytheon Company | CO2 tea laser |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1299606B (en) * | 1963-06-26 | 1969-07-24 | Engel Geb Jatsch Anna | Process for the production of very effective, abrasion-resistant catalysts for cleaning engine exhaust gases |
| GB1171581A (en) * | 1967-02-14 | 1969-11-19 | Kachita Company Ltd | A Method of Preparing a Granular Oxidising Catalyst for Preventing Air Contamination by Carbon Monoxide |
| DE3148570C2 (en) * | 1981-12-08 | 1991-02-14 | Eltro GmbH, Gesellschaft für Strahlungstechnik, 6900 Heidelberg | Electrically excited CO ↓ ↓ 2 ↓ ↓ laser |
-
1984
- 1984-11-23 FR FR8417886A patent/FR2575869B1/en not_active Expired
-
1985
- 1985-11-21 DE DE8585402263T patent/DE3572754D1/en not_active Expired
- 1985-11-21 EP EP85402263A patent/EP0188138B1/en not_active Expired
-
1987
- 1987-12-07 US US07/129,528 patent/US4815092A/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4547886A (en) * | 1981-09-25 | 1985-10-15 | United Technologies Corporation | Catalyzed sealed-off CO2 laser |
| US4617668A (en) * | 1982-07-02 | 1986-10-14 | Raytheon Company | CO2 tea laser |
Non-Patent Citations (2)
| Title |
|---|
| C. Willis et al., "Sealed Tea CO2 Lasers with External Control of Gas Chemistry", Appl. Phsy. Letters, vol. 31, No. 2, (15 Jul. 1977), pp. 84-86. |
| C. Willis et al., Sealed Tea CO 2 Lasers with External Control of Gas Chemistry , Appl. Phsy. Letters, vol. 31, No. 2, (15 Jul. 1977), pp. 84 86. * |
Cited By (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4905249A (en) * | 1989-01-06 | 1990-02-27 | Applied Photonics, Inc. | Catalytic converter |
| DE3923745A1 (en) * | 1989-07-18 | 1991-01-31 | Eltro Gmbh | LASER DEVICE WITH RAMAN CELL |
| US6125131A (en) * | 1994-10-13 | 2000-09-26 | Advanced Technology Materials, Inc. | Laser system utilizing sorbent-based gas storage and delivery system |
| WO1996022825A1 (en) * | 1995-01-27 | 1996-08-01 | Purafil, Inc. | Improved fiber filter and methods of use thereof |
| US5942323A (en) * | 1995-01-27 | 1999-08-24 | Purafil, Inc. | Fiber filter and methods of use thereof |
| US6265024B1 (en) | 1995-01-27 | 2001-07-24 | Purafil, Inc. | Fiber filter and methods of use thereof |
| US6605558B2 (en) | 1997-02-11 | 2003-08-12 | Fred Klatte | Composition for producing chlorine dioxide |
| US6635230B2 (en) | 1997-02-11 | 2003-10-21 | Fred Klatte | Method for producing chlorine dioxide |
| US6940886B2 (en) * | 2000-03-31 | 2005-09-06 | Mitsubishi Denki Kabushiki Kaisha | Laser oscillator |
| US20030179798A1 (en) * | 2002-03-25 | 2003-09-25 | Fanuc Ltd. | Laser oscillator |
| US7149237B2 (en) * | 2002-03-25 | 2006-12-12 | Fanuc Ltd | Laser oscillator |
| US20040126402A1 (en) * | 2002-09-13 | 2004-07-01 | Ica Trinova Llc | Method and composition for attracting arthropods by volatilizing an acid |
| US20040051080A1 (en) * | 2002-09-13 | 2004-03-18 | Ica Trinova, Llc | Composition and method for producing carbon dioxide |
| US7347994B2 (en) | 2002-09-13 | 2008-03-25 | Ica Trinova, Llc | Method and composition for attracting arthropods by volatilizing an acid |
| US20080138372A1 (en) * | 2002-09-13 | 2008-06-12 | Ica Trinova Llc | Method and composition for attracting arthropods by volatilizing an acid |
| US7922992B2 (en) | 2002-09-13 | 2011-04-12 | Ica Trinova, Llc | Composition and method for producing carbon dioxide |
| US8709396B2 (en) | 2002-09-13 | 2014-04-29 | Premark Feg L.L.C. | Method and composition for attracting arthropods by volatizing an acid |
| US7758836B1 (en) | 2009-04-14 | 2010-07-20 | Huggins Ronald G | System and method for removing sulfur-containing contaminants from indoor air |
| US9382116B2 (en) | 2013-01-10 | 2016-07-05 | Ica Trinova, Llc | Mixtures for producing chlorine dioxide gas in enclosures and methods of making the same |
| US10850981B2 (en) | 2017-04-25 | 2020-12-01 | Ica Trinova, Llc | Methods of producing a gas at a variable rate |
| US11518676B2 (en) | 2017-04-25 | 2022-12-06 | Ica Trinova Llc | Methods of producing a gas at a variable rate |
| US11912568B2 (en) | 2018-03-14 | 2024-02-27 | Ica Trinova, Llc | Methods of producing a gas at a controlled rate |
| US12221341B2 (en) | 2018-03-14 | 2025-02-11 | Ica Trinova, Llc | Methods of producing a gas at a controlled rate |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0188138B1 (en) | 1989-08-30 |
| EP0188138A1 (en) | 1986-07-23 |
| FR2575869B1 (en) | 1987-07-10 |
| FR2575869A1 (en) | 1986-07-11 |
| DE3572754D1 (en) | 1989-10-05 |
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Legal Events
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| REMI | Maintenance fee reminder mailed | ||
| LAPS | Lapse for failure to pay maintenance fees | ||
| FP | Lapsed due to failure to pay maintenance fee |
Effective date: 19930321 |
|
| STCH | Information on status: patent discontinuation |
Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362 |